JPH05329498A - Method for removing and recovering aluminum in sludge in water purification - Google Patents
Method for removing and recovering aluminum in sludge in water purificationInfo
- Publication number
- JPH05329498A JPH05329498A JP4141399A JP14139992A JPH05329498A JP H05329498 A JPH05329498 A JP H05329498A JP 4141399 A JP4141399 A JP 4141399A JP 14139992 A JP14139992 A JP 14139992A JP H05329498 A JPH05329498 A JP H05329498A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- water
- hydrochloric acid
- aluminum
- sent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、浄水場で河川からの
水の濁り成分を凝集剤の添加で沈殿させることにより生
成した汚泥(本明細書全体を通して「浄水汚泥」とい
う)中の上記凝集剤に由来するアルミニウム分を、浄水
汚泥から除去および回収する方法に関する。BACKGROUND OF THE INVENTION The present invention relates to the above coagulation in sludge (referred to as "purified water sludge" throughout the specification) produced by precipitating turbid components of water from a river at a water purification plant by adding a coagulant. The present invention relates to a method for removing and recovering aluminum content derived from the agent from purified water sludge.
【0002】[0002]
【従来技術および解決すべき課題】浄水汚泥は、SiO
2 、Al2 O3 、Fe2 O3 を主成分とする粘土であ
り、現在これは埋立投棄により処分されている。しか
し、近年、埋め立て処分場の確保がますます困難になる
状況にあり、浄水汚泥を他の用途に有効利用する方策が
切望されている。Prior Art and Problems to be Solved
It is a clay composed mainly of 2 , Al 2 O 3 and Fe 2 O 3 , which is currently disposed of by landfill. However, in recent years, it is becoming more and more difficult to secure a landfill disposal site, and a measure for effectively utilizing the purified water sludge for other purposes is desired.
【0003】浄水場で河川水に添加される凝集剤は、水
道用ポリ塩化アルミニウム(PAC)JIS K147
5(1978)である。したがって、この凝集剤を含む
浄水汚泥をそのまま農耕用の土壌として使用すると、P
AC中の可溶性アルミニウムがリン酸肥料と反応し、そ
の結果土壌がリン欠乏土壌となり、作物の成育を阻害す
る。そのため、浄水汚泥からPACを除去する技術が必
要である。The coagulant added to river water at a water purification plant is polyaluminum chloride (PAC) JIS K147 for water supply.
5 (1978). Therefore, if the purified water sludge containing this coagulant is used as it is as soil for agriculture, P
Soluble aluminum in AC reacts with phosphate fertilizers, resulting in soils that are phosphorus deficient and inhibit crop growth. Therefore, a technique for removing PAC from purified water sludge is required.
【0004】従来より、浄水汚泥処理において、硫酸ア
ルミニウムを回収する方法はいくつかあるが、塩化アル
ミニウム系凝集剤を回収する例はない。Conventionally, there are several methods of recovering aluminum sulfate in the treatment of purified water sludge, but there is no example of recovering an aluminum chloride-based coagulant.
【0005】また、浄水汚泥を乾燥・焼成することによ
り、可溶性アルミニウムを固定し、処理後の汚泥を土壌
として有効利用する方法もあるが、この方法では焼成用
燃料の消費量が大きい上にアルミニウムが回収できない
という難点がある。There is also a method in which soluble aluminum is fixed by drying and firing purified water sludge and the treated sludge is effectively used as soil. However, this method consumes a large amount of fuel for firing, and aluminum is used. However, there is a drawback that it cannot be collected.
【0006】この発明の目的は、浄水汚泥中に含まれる
ポリ塩化アルミニウム凝集剤の可溶性アルミニウムを除
去して、浄化汚泥を農作物育成用の土壌として有効利用
し、かつ回収アルミニウムを凝集剤として再使用する方
法を提供することにある。An object of the present invention is to remove soluble aluminum of polyaluminum chloride flocculant contained in purified water sludge, effectively utilize the purified sludge as soil for growing crops, and reuse recovered aluminum as flocculant. To provide a way to do.
【0007】[0007]
【課題を解決するための手段】この発明は、上記の目的
を達成すべく工夫されたもので、浄水汚泥を塩酸ないし
希塩酸で洗浄することにより、汚泥中の可溶性アルミニ
ウムを回収することを特徴とする浄水汚泥中のアルミニ
ウム除去および回収方法である。The present invention has been devised to achieve the above object and is characterized by recovering soluble aluminum in sludge by washing purified water sludge with hydrochloric acid or dilute hydrochloric acid. This is a method for removing and recovering aluminum from purified water sludge.
【0008】処理すべき浄水汚泥は、濃縮槽で濃縮され
ると同時にまたは濃縮された後、もしくは、脱水機で脱
水されると同時にまたは脱水された後、塩酸ないし希塩
酸で洗浄される。脱水と同時もしくは脱水後の場合に
は、好ましくは希塩酸が用いられる。[0008] The purified water sludge to be treated is washed with hydrochloric acid or dilute hydrochloric acid at the same time as it is concentrated in a concentrating tank or after being concentrated, or at the same time as being dehydrated by a dehydrator or after being dehydrated. Simultaneously with or after dehydration, dilute hydrochloric acid is preferably used.
【0009】[0009]
【実施例】つぎに、この発明の実施例について添付図面
を参照して具体的に説明する。Embodiments of the present invention will now be described in detail with reference to the accompanying drawings.
【0010】浄水場において、河川から取水した水は殺
菌槽(1) に導かれ、この水に塩素が加えられ殺菌が施さ
れる。ついでこの水は攪拌池(2) へ導かれ、ここで水に
凝集剤として水道用ポリ塩化アルミニウムが添加され、
水が攪拌される。この水はついでフロック形成池(3) へ
送られて、凝集剤によってフロックが形成され、次にフ
ロックを含む水は沈殿池(4) へ送られ、静置される。そ
の結果、水中の濁り成分が沈殿させられ、浄水汚泥が生
成する。この汚泥はついで汚泥濃縮槽(5) へ送られて濃
縮され、さらに濃縮汚泥は、脱水機(6) に送られる。脱
水機(6) には中和用の希塩酸が注入され、脱水機(6) の
駆動により汚泥の脱水と同時に汚泥が希塩酸で洗浄され
る。In the water purification plant, the water taken from the river is guided to the sterilization tank (1), and chlorine is added to this water to sterilize it. This water is then led to a stirring pond (2), where water polyaluminum chloride is added as a coagulant to the water,
The water is stirred. This water is then sent to the floc pond (3) where flocs are formed by the flocculant, then the water containing flocs is sent to the settling pond (4) and allowed to stand. As a result, turbid components in water are precipitated and purified water sludge is produced. This sludge is then sent to the sludge thickening tank (5) for concentration, and the concentrated sludge is further sent to the dehydrator (6). Diluted hydrochloric acid for neutralization is injected into the dehydrator (6), and the sludge is dehydrated and simultaneously washed with diluted hydrochloric acid by driving the dehydrator (6).
【0011】この酸洗浄により、汚泥中の可溶性アルミ
ニウムが除去され、得られた洗浄汚泥が農作物育成用の
土壌として有効利用される。他方、回収されたアルミニ
ウムは処理装置(7) で処理され、凝集剤として再利用さ
れる。By this acid washing, soluble aluminum in the sludge is removed, and the obtained washed sludge is effectively used as soil for growing agricultural products. On the other hand, the recovered aluminum is treated in the treatment device (7) and reused as a flocculant.
【0012】沈殿池(4) で得られた濁り除去水は急速濾
過池(8) で濾過された後、浄水池(9) に貯えられる。The turbidity-removed water obtained in the sedimentation basin (4) is filtered in the rapid filtration basin (8) and then stored in the water purification basin (9).
【0013】処理前の浄水脱水汚泥中の可溶性アルミニ
ウムは乾燥汚泥1kg当り45,000mg程度であ
り、一般土壌では500mg程度である。そのため、浄
水汚泥中の可溶性アルミニウムの含有量を一般土壌の値
まで下げるには、浄水汚泥中の可溶性アルミニウムを9
9%近くまで除去する必要がある(この場合、添加した
ポリ塩化アルミニウム凝縮剤からのアルミニウムはほと
んど回収されることになる)。上記の如く、ポリ塩化ア
ルミニウム凝集剤を用いた脱水汚泥からの可溶性アルミ
ニウムの希釈酸による洗浄除去を行なった。脱水汚泥を
0.5N塩酸で濾紙上で洗浄した後、濾紙上の汚泥を乾
燥し、可溶性アルミニウムを溶出分析したところ、1k
g当り500mg以下となった。Soluble aluminum in the purified water dewatered sludge before treatment is about 45,000 mg per kg of dry sludge, and about 500 mg in general soil. Therefore, in order to reduce the content of soluble aluminum in purified water sludge to the value of general soil, 9% soluble aluminum in purified water sludge should be used.
It should be removed to close to 9% (in which case most of the aluminum from the added polyaluminum chloride condensing agent will be recovered). As described above, the soluble aluminum from the dehydrated sludge using the polyaluminum chloride flocculant was washed and removed with a dilute acid. After washing the dehydrated sludge on the filter paper with 0.5N hydrochloric acid, the sludge on the filter paper was dried and the soluble aluminum was eluted and analyzed.
It became 500 mg or less per gram.
【0014】[0014]
【発明の効果】この発明によれば、浄水汚泥を塩酸ない
し希塩酸で洗浄することにより、浄水汚泥中に含まれる
ポリ塩化アルミニウム凝集剤の可溶性アルミニウムを除
去して、浄化汚泥を農作物育成用の土壌として有効利用
し、かつ回収アルミニウムを凝集剤として再使用するこ
とができる。According to the present invention, the purified sludge is washed with hydrochloric acid or dilute hydrochloric acid to remove the soluble aluminum of the polyaluminum chloride flocculant contained in the purified water sludge, and the purified sludge is used as a soil for growing agricultural crops. The recovered aluminum can be reused as a flocculant.
【図1】この発明の実施例を示すフローチャートであ
る。FIG. 1 is a flow chart showing an embodiment of the present invention.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 太田 完志 大阪市此花区西九条5丁目3番28号 日立 造船株式会社内 (72)発明者 平田 直子 大阪市此花区西九条5丁目3番28号 日立 造船株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kanshi Ota, 5-3-8 Nishi Kujo, Konohana-ku, Osaka City, Hitachi Shipbuilding Co., Ltd. (72) Naoko Hirata 5-28, Nishi Kujo, Konohana-ku, Osaka Issue Hitachi Shipbuilding Co., Ltd.
Claims (1)
ことにより、汚泥中の可溶性アルミニウムを回収するこ
とを特徴とする浄水汚泥中のアルミニウム除去および回
収方法。1. A method for removing and recovering aluminum in purified water sludge, which comprises recovering soluble aluminum in the sludge by washing the purified water sludge with hydrochloric acid or dilute hydrochloric acid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4141399A JP2952732B2 (en) | 1992-06-02 | 1992-06-02 | Method for removing and recovering aluminum in purified water sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4141399A JP2952732B2 (en) | 1992-06-02 | 1992-06-02 | Method for removing and recovering aluminum in purified water sludge |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05329498A true JPH05329498A (en) | 1993-12-14 |
JP2952732B2 JP2952732B2 (en) | 1999-09-27 |
Family
ID=15291100
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4141399A Expired - Lifetime JP2952732B2 (en) | 1992-06-02 | 1992-06-02 | Method for removing and recovering aluminum in purified water sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2952732B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106977035A (en) * | 2017-05-24 | 2017-07-25 | 广西碧清源环保科技有限公司 | A kind of processing for mixing waste emulsified mixture, retracting device |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE0102222D0 (en) * | 2001-06-21 | 2001-06-21 | Chematur Eng Ab | Process and plant for treatment of waste |
KR101281145B1 (en) * | 2012-11-15 | 2013-07-02 | 윤호석 | A method for aluminium chloride from filtration plant sludge |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55167099A (en) * | 1979-06-15 | 1980-12-26 | Miura Eng Internatl Kk | Treatment of flocculated and precipitated sludge |
-
1992
- 1992-06-02 JP JP4141399A patent/JP2952732B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55167099A (en) * | 1979-06-15 | 1980-12-26 | Miura Eng Internatl Kk | Treatment of flocculated and precipitated sludge |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106977035A (en) * | 2017-05-24 | 2017-07-25 | 广西碧清源环保科技有限公司 | A kind of processing for mixing waste emulsified mixture, retracting device |
Also Published As
Publication number | Publication date |
---|---|
JP2952732B2 (en) | 1999-09-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5914040A (en) | Process for the purification of a medium containing organic waste | |
CA2493615C (en) | Hog manure treatment system | |
CN109879539A (en) | A kind of waste water of basic printing and dyeing circular regeneration processing method | |
JP3879136B2 (en) | Dephosphorization equipment | |
KR100467396B1 (en) | Discharged water treatment method | |
JPH05329498A (en) | Method for removing and recovering aluminum in sludge in water purification | |
JP4467897B2 (en) | Phosphorus-containing organic sewage treatment equipment | |
JP3277832B2 (en) | Method for treating phosphorus recovered from sewage treatment water | |
CN106277630A (en) | High skilful production waste decoloration treatment method | |
CN109205916A (en) | The processing method of wash water is sprayed in production process of activated carbon | |
JPH09187797A (en) | Treatment method for sludge | |
RU99111462A (en) | METHOD OF WASTEWATER TREATMENT | |
GB1368806A (en) | Treatment of industrial and domestic waste waters | |
JPS55167099A (en) | Treatment of flocculated and precipitated sludge | |
RU2158327C1 (en) | Method of treatment of excessive circulating water of cardboard production for its reuse | |
JPS58112086A (en) | Purification of waste water contg. biologically difficulty-decomposable substance | |
JPH0316700A (en) | Method for dehydrating sludge and chemicals used therefor | |
Amirtharajah | Coagulation: Rejuvenation for a classical process | |
Jones | Wastewater flocculating agent. | |
JPS63214389A (en) | Treatment of organic sewage | |
JP2000093706A (en) | Flocculation precipitation treating equipment | |
SU676562A1 (en) | Method of purifying water from aquatic plants | |
KR940011522B1 (en) | Method for treatment of waste water using sea water | |
JPS62110796A (en) | Treatment of night soil | |
JPH0321398A (en) | Treatment of organic sludge |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19990525 |